JPS5811558B2 - Packing material consisting of a foil-like material with flow surfaces for "troughs" for mass and heat exchange - Google Patents

Packing material consisting of a foil-like material with flow surfaces for "troughs" for mass and heat exchange

Info

Publication number
JPS5811558B2
JPS5811558B2 JP53047167A JP4716778A JPS5811558B2 JP S5811558 B2 JPS5811558 B2 JP S5811558B2 JP 53047167 A JP53047167 A JP 53047167A JP 4716778 A JP4716778 A JP 4716778A JP S5811558 B2 JPS5811558 B2 JP S5811558B2
Authority
JP
Japan
Prior art keywords
flow surface
flow
liquid
filler
smooth
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP53047167A
Other languages
Japanese (ja)
Other versions
JPS5415554A (en
Inventor
マツクス・フーベル
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sulzer AG
Original Assignee
Sulzer AG
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sulzer AG filed Critical Sulzer AG
Publication of JPS5415554A publication Critical patent/JPS5415554A/en
Publication of JPS5811558B2 publication Critical patent/JPS5811558B2/en
Expired legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F25/00Component parts of trickle coolers
    • F28F25/02Component parts of trickle coolers for distributing, circulating, and accumulating liquid
    • F28F25/08Splashing boards or grids, e.g. for converting liquid sprays into liquid films; Elements or beds for increasing the area of the contact surface
    • F28F25/087Vertical or inclined sheets; Supports or spacers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/32Packing elements in the form of grids or built-up elements for forming a unit or module inside the apparatus for mass or heat transfer
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322Basic shape of the elements
    • B01J2219/32203Sheets
    • B01J2219/3221Corrugated sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322Basic shape of the elements
    • B01J2219/32203Sheets
    • B01J2219/32213Plurality of essentially parallel sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322Basic shape of the elements
    • B01J2219/32203Sheets
    • B01J2219/32213Plurality of essentially parallel sheets
    • B01J2219/3222Plurality of essentially parallel sheets with sheets having corrugations which intersect at an angle different from 90 degrees
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322Basic shape of the elements
    • B01J2219/32203Sheets
    • B01J2219/32224Sheets characterised by the orientation of the sheet
    • B01J2219/32227Vertical orientation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322Basic shape of the elements
    • B01J2219/32203Sheets
    • B01J2219/32237Sheets comprising apertures or perforations
    • B01J2219/32244Essentially circular apertures
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322Basic shape of the elements
    • B01J2219/32203Sheets
    • B01J2219/32248Sheets comprising areas that are raised or sunken from the plane of the sheet
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322Basic shape of the elements
    • B01J2219/32203Sheets
    • B01J2219/32255Other details of the sheets
    • B01J2219/32258Details relating to the extremities of the sheets, such as a change in corrugation geometry or sawtooth edges
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/324Composition or microstructure of the elements
    • B01J2219/32408Metal
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/324Composition or microstructure of the elements
    • B01J2219/32483Plastics
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S261/00Gas and liquid contact apparatus
    • Y10S261/72Packing elements

Description

【発明の詳細な説明】 本発明は2種の流動性の媒質の間、特に液体とガスとの
間の物質および熱交換のための浴用の、流動面を有する
フォイル状材料から成る充填材に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a filler consisting of a foil-like material with a flow surface for baths for the exchange of substances and heat between two fluid media, in particular between a liquid and a gas. .

塔充填材は大多数のばら積みされた、例へばラツシヒリ
ングのような同じ充填材から成るか、またはバッキング
材料とも称される、整列された構造を有する取付は要素
から構造されることができる。
The column packing can consist of a large number of bulk packed, identical packing materials, for example Luschig rings, or the mounting can be constructed from elements with an aligned structure, also referred to as backing material.

本発明はフォイル状材料から成る充填材の流動面を好適
に形成することによって物質および熱交換を促進する課
題を基調とする。
The invention is based on the problem of promoting mass and heat exchange through a suitable formation of flow surfaces in a filler made of foil-like material.

この課題は本発明に基づき、流動面は平滑な部分と波型
溝付きの部分とを交互に有し、その場合側々の部分は夫
々少なくとも5mmの高さにわたって延びていることに
よって解決される。
This problem is solved according to the invention in that the flow surface has alternating smooth and corrugated sections, the lateral sections each extending over a height of at least 5 mm. .

波型溝付きとは本発明においては導溝によるまたは例へ
ば魚骨模様のような模様の刻み付けによる薄板表面のケ
バ立てのことである。
In the present invention, wavy grooving refers to the raising of the surface of a thin plate by guiding grooves or by carving a pattern such as a fishbone pattern, for example.

整列された構造を有する取付は要素として充填材を形成
する場合流動面上には平滑な部分と微少波型溝付きの部
分とが液体の流下線方向に交互に配置されている。
When a mounting with an aligned structure forms a filler as an element, smooth sections and sections with micro-wavy grooves are arranged alternately on the flow surface in the direction of the flow line of the liquid.

取付は要素が基軸線に平行に配置された、接触する、折
り目を付けられた薄板から成っておりかつ微少波型溝付
きが導溝から成っている場合、微少波型溝付き部分の導
溝は基軸線に対し優先的に、折り目の相応する角の反対
の前置符号を有する角度を形成する。
The mounting consists of contacting, creased thin plates arranged parallel to the basic axis and the microcorrugated grooved part consists of a guiding groove, if the microcorrugated grooved part consists of a guiding groove. preferentially forms an angle with the cardinal axis having the opposite prefix of the corresponding corner of the fold.

折り目を付けられた流動面から成る取付は要素の場合、
液体は主として折り目によって形成された谷底を流れ、
すなわち液体のカナリゼーションが発生し、かつ液体は
流動面を均等には流動しない。
For elements whose mounting consists of a creased flow surface,
The liquid mainly flows through the valley bottom formed by the folds,
That is, canalization of the liquid occurs and the liquid does not flow uniformly on the flow surface.

導溝として微少波型溝を形成する場合導溝は水平の方向
に延びることができる。
When forming a minute wave-type groove as a guide groove, the guide groove can extend in a horizontal direction.

ただし本発明の有利な形成によれば微少導溝と基軸線と
の間の角度は15−90°の間に、また折れ目と基軸線
との間の角度は約15−60°の範囲にある。
However, according to an advantageous embodiment of the invention, the angle between the microchannel and the basic axis is between 15 and 90°, and the angle between the fold and the basic axis is in the range of approximately 15-60°. be.

この場合には流動表面上の液体の側方への拡張は流動谷
の中で有効になる剪断力によってなお強化される。
In this case, the lateral expansion of the liquid on the flow surface is further enhanced by the shear forces prevailing in the flow troughs.

本発明が包括するすべての充填材型においては次の過程
が生ずる: 液体は流動面上をフィルムとして流下する。
In all filler types covered by the invention, the following process occurs: The liquid flows down as a film on the flow surface.

物質および熱交換はガス相から液体フィルムの中への、
もしくはこれと反対の拡散過程によって行われる。
Mass and heat exchange from the gas phase into the liquid film,
Or by the opposite process of diffusion.

これらの過程はいわゆる2−フィルム理論(Zwei−
Filmtheorie)によって行われる。
These processes are explained by the so-called two-film theory (Zwei-
Filmtheorie).

ガス流の核から液体の核の中へ達するため分子が必要と
する時間は2個の部分ステップから構成される。
The time required for a molecule to pass from the core of the gas stream into the core of the liquid consists of two partial steps.

最初に分子はガス流の核から相界面に達する。First the molecules reach the phase interface from the core of the gas stream.

第2のステップにおいて分子は相界面から液体の核の中
へ達する。
In the second step the molecules pass from the phase interface into the liquid core.

本発明によれば第2のステップが全体的に促進される。According to the invention, the second step is entirely facilitated.

液体のフィルムの厚さは、流動面の微細な波形溝を形成
した部分の上では平滑な部分の上よりもずっと厚く、そ
の場合平滑な部分の上にはフィルムが形成されず、液体
の細い流れができる。
The thickness of the liquid film is much thicker on the part of the flow surface with fine wavy grooves than on the smooth part, in which case no film is formed on the smooth part, and the thin It creates a flow.

1つの区域から他の区域へ液体が移動する際には、フィ
ルムの厚さが変化しかつ新しい液体の表面が生じる。
As liquid moves from one area to another, the film thickness changes and new liquid surfaces are created.

その際粒子は液体の核の流れから表面に、もしくはこれ
と反対に移動して到達する。
Particles then move from the flow of the liquid core to the surface or vice versa.

この機械的運動は、拡散による分子の運動よりも数倍も
迅速である。
This mechanical movement is several times faster than the movement of molecules due to diffusion.

それによって濃度の差異または温度の差異が、単に拡散
だけによるのではなく、個々の液体粒子の迅速な運動に
より、なくなるように調整される。
Differences in concentration or temperature are thereby compensated for by the rapid movement of the individual liquid particles and not simply by diffusion.

それによって物質または熱交換が改良される。Mass or heat exchange is thereby improved.

以下図面の実施例によって本発明を詳述する。The present invention will be explained in detail below with reference to embodiments of the drawings.

第1図の流動面1は尖角2aと谷底2bとを有する粗折
れ目を有する。
The flow surface 1 in FIG. 1 has a rough fold with a cusp 2a and a trough 2b.

折れ目付けの概念は本発明においては歯型および波型の
断面形成のことである。
The concept of scoring refers to tooth-shaped and wave-shaped cross-sectional formations in the present invention.

金属、例へば銅、ステンレススチールまたはモネル合金
またはプラスチックから成ることができる流動面は基軸
線に対し垂直に交互に平滑な部分と微少波形溝付きの部
分3と4とに区分されている。
The flow surface, which can be made of metal, for example copper, stainless steel or Monel alloy or plastic, is divided perpendicular to the basic axis into alternating smooth and micro-corrugated sections 3 and 4.

微少溝5は部分4の中に、折れ目の傾斜角に反対の角度
を成して配置されている。
The microgroove 5 is arranged in the part 4 at an angle opposite to the angle of inclination of the fold.

波型溝の長さおよび波型溝の高さは0.3−3mmの大
きさであるのが有利である。
Advantageously, the length of the corrugated grooves and the height of the corrugated grooves measure 0.3-3 mm.

微少溝と基軸線との間の角度は15−90°、また折れ
目と基軸線との間の角度は15−60°であるのが有利
であり、その場合前者の角度は後者の角度に反対の前置
符号を有する。
Advantageously, the angle between the microgroove and the cardinal axis is 15-90°, and the angle between the fold and the cardinal axis is 15-60°, the former angle being equal to the latter angle. have opposite prefixes.

平滑な部分3は若干数の孔6を備えている。The smooth part 3 is provided with a number of holes 6.

孔は約4mmの大きさの直径を有しかつ全部で全流動面
の5−20%以上を占めないのが有利である。
Advantageously, the holes have a diameter of approximately 4 mm and in total do not occupy more than 5-20% of the total flow surface.

第2図に表わされた、流動面の実施型は微少波型溝付き
の部分4も距離をおいて穿孔されている点を除けば第1
図と一致している。
The embodiment of the flow surface represented in FIG.
Consistent with the diagram.

第3図は平滑な部分3′および微少波型溝付きの部分4
′が基軸線に対し垂直ではなく角度を成して配置されて
いる流動面の実施型を示す。
Figure 3 shows a smooth part 3' and a part 4 with minute wave-shaped grooves.
' shows an embodiment of the flow surface which is arranged not perpendicularly but at an angle to the base axis.

第4図には展開された流動面における流動図が図形的に
示され、かつ第4a図には第4図の■a−■a断面線に
沿う側面図が表わされている。
FIG. 4 graphically shows a flow diagram in the developed flow plane, and FIG. 4a shows a side view along the cross-sectional line ``a''--``a'' in FIG. 4.

部分3″は微少波型溝5″を有し、一方部分4″は平滑
な表面を有しかつ微少波型溝付きの部分と同じように数
個の孔6″を有する。
The part 3'' has micro-corrugated grooves 5", while the part 4" has a smooth surface and, like the micro-corrugated part, has several holes 6".

流動図は、液体はフィルムとして部分3″を経て流下し
、一方平滑な部分上を液体は小川になって流れながら孔
6″によって少なくとも1部分側方へ誘導されることを
表わしている。
The flow diagram shows that the liquid flows down through the section 3'' as a film, while on the smooth section the liquid flows in streams and is guided at least partially laterally by the holes 6''.

第5図には第1図ないし第3図において形成され得る流
動面1を示す。
FIG. 5 shows a flow surface 1 that can be formed in FIGS. 1 to 3. In FIG.

この流動面は接続して従列されかつ1個の取付は要素に
併合されかつ次いでシリンダー状の塔の交換部分に据付
けられる順序に表わされており、その場合取付は要素を
形成する流動面の1部分だけが表わされている。
The flow surfaces are connected and cascaded and one fitting is shown in the order in which it is merged into the element and then installed in the replacement part of the cylindrical column, where the fittings are connected to the flow surfaces forming the element. Only a portion of is represented.

取付は要素は平行の、折れ目を付けられていない流動面
から構成されることもできるだろうが、その場合隣接す
る層の距離は公知の方法でスペーサにより確保される。
The mounting elements could also consist of parallel, unscorched flow surfaces, in which case the distance between adjacent layers would be ensured by spacers in a known manner.

第6図はコイル成形体の製造のため、コイル状に巻かれ
た、魚骨状に折り曲げられた流動面を形成するバンド7
の遠近図を示す。
Fig. 6 shows a band 7 that is wound into a coil shape and forms a fluid surface bent into a fishbone shape for the production of a coil molded body.
shows a perspective view.

流動面は微少波型溝付けされた部分3と平滑な部分4と
に区分されている。
The flow surface is divided into a micro-wavy grooved section 3 and a smooth section 4.

コイル成形体は折れ目を付けられていないバンドから成
ることもでき、その場合隣接する層の間隔は公知の方法
でスペーサによって保持される。
The coiled body can also consist of an unscored band, in which case the distance between adjacent layers is maintained by spacers in a known manner.

第7図には微少波型溝を付けられた部分9と平滑な部分
10とを有し、平滑な部分は孔11を有している。
In FIG. 7, it has a part 9 with minute wavy grooves and a smooth part 10, and the smooth part has holes 11.

ラツシヒリングとして形成された充填材8にして、物質
または熱交換部分はこの種充填材のばら積みを含んでい
る塔に利用される充填材が表わされている。
The packing 8, which is designed as a Luschig ring, represents a packing used in columns in which the mass or heat exchange part contains bulk packings of this type.

充填材はサドル、ウェブ付のリングなどのようなばら積
み充填材として公知の他の形成を有することもできよう
The filler could also have other configurations known as bulk fillers, such as saddles, rings with webs, etc.

第8図には塔16の交換部分の1部分15が表わされ、
この部分は夫々相互に90°だけ偏位して配置された3
個の取付は要素17,18.19を含んでいる。
In FIG. 8, one section 15 of the replacement part of the column 16 is represented,
These parts are each arranged 3
The installation includes elements 17, 18, and 19.

この場合取付は要素は本発明により形成された流動面の
層から構成されている。
In this case the mounting element consists of a layer of flow surface formed according to the invention.

(第5図参照)。(See Figure 5).

取付は要素の下方部分にはカラーとして形成された誘導
要素20が固定され、この誘導要素は充填材と塔壁との
間のリング間隙を緊塞しかつ、内壁に沿って流下する液
体を各取付は要素の下側において内方へ誘導する作用を
成す。
The mounting is such that in the lower part of the element a guiding element 20 in the form of a collar is fixed, which closes the annular gap between the packing material and the column wall and directs the liquid flowing down along the inner wall. The attachment acts inwardly on the underside of the element.

かかるカラーを取付は要素の種々の高さに配置すること
もできる。
Mounting of such collars can also be arranged at various heights of the element.

最下方の取付は要素に接続する、塔の蒸発部分内へ液体
を、塔横断面にわたって均等に分配して誘導するためこ
の取付は要素の薄板の最下側は尖角21に終っている。
The lowermost attachment connects to the element, and this attachment terminates in a cusp 21 on the lowermost side of the lamina of the element in order to guide the liquid evenly distributed over the column cross-section into the evaporation section of the column.

塔16の中には勿論、前記のようなコイル成形体を取付
は要素または充填材ばら積みとして装入することもでき
る。
Of course, the column 16 can also be loaded with a coiled body of the type described above as a mounting element or bulk filler.

例へば1mおよびこれ以上の大なる塔直径の場合には取
付は要素は従列配置された数個の部分から成ることがで
きる。
In the case of large column diameters, for example 1 m and more, the installation element can consist of several parts arranged one after the other.

これらの個々の部分は塔外波によって結合保持される。These individual parts are held together by external waves.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は流動面の遠近図、第1a図は流動面の細部の拡
大図、第2図と第3図は流動面の他の実施型の図、第4
図は展開された流動面用の流動バンドの図形、第4a図
は第4図の■a−■a断面線に沿う側面図、第5図、第
6図、第7図は併行な流動面から形成された取付は要素
、ならびにコイル状に巻かれたバンドからおよび充填材
ばら積みを有する塔の中に使用されるような充填材から
成る取付は要素の遠近図、第8図は第5図に従って形成
した3個の取付は要素を内蔵する塔の一部を示す。 図面の主な符号の説明、1:流動面、2a:尖角、2b
:谷底、3,3′、3″、10:平滑な部分、4.4′
、4″、9:微少波型溝付けの部分、6.6″、11:
孔、8:充填材、16:塔、17゜18.19:取付は
要素。
1 is a perspective view of the flow surface, FIG. 1a is an enlarged view of a detail of the flow surface, FIGS. 2 and 3 are views of other embodiments of the flow surface, FIG.
The figure shows the diagram of the flow band for the developed flow surface, Figure 4a is a side view along the cross-sectional line ■a-■a in Figure 4, and Figures 5, 6, and 7 are parallel flow surfaces. Figure 8 is a perspective view of the element; The three fittings formed according to the above designate part of the tower containing the elements. Explanation of main symbols in the drawings: 1: Flow surface, 2a: Point angle, 2b
: Valley bottom, 3,3', 3'', 10: Smooth part, 4.4'
, 4″, 9: Microwave grooved part, 6.6″, 11:
Hole, 8: Filler, 16: Tower, 17° 18.19: Mounting element.

Claims (1)

【特許請求の範囲】 12つの流動性の媒質の間、特に液体とガスとの間の物
質および熱交換のための浴用の、流動面を有する箔状の
材料から成る充填材において、前記流動面は交互に平滑
な部分と微細な波形溝を形成した部分とを有し、その場
合側々の部分は少なくとも5mmの高さにわたって延び
ていることを特徴とする充填材。 2、特許請求の範囲第1項に記載する充填材において、
前記流動面は少なくとも前記の平滑な部分において孔を
あけられていることを特徴とする充填材。 3 特許請求の範囲第1項に記載する充填材において、
前記の微細な波形溝が条溝から成ることを特徴とする充
填材。 4 特許請求の範囲第1項に記載する充填材において、
整列された構造を有する取付は要素として充填材を形成
する場合には、前記流動面上に前記の平滑な部分と前記
の微細な波形溝を形成した部分とが液体の流下線の方向
に交互に配置されていることを特徴とする充填材。
Claims: 1. A filling consisting of a foil-like material with a flow surface for baths for the exchange of substances and heat between two flowable media, in particular between a liquid and a gas, wherein said flow surface is Filling material characterized in that it has alternating smooth sections and sections with finely corrugated grooves, the lateral sections extending over a height of at least 5 mm. 2. In the filler described in claim 1,
A filler characterized in that the flow surface is perforated at least in the smooth portion. 3 In the filler described in claim 1,
A filling material characterized in that the fine wave-shaped grooves described above are composed of grooves. 4 In the filler described in claim 1,
When a mounting with an aligned structure forms a filler as an element, the smooth part and the part formed with the fine wavy grooves on the flow surface alternate in the direction of the flow line of the liquid. A filling material characterized by being arranged in.
JP53047167A 1977-05-12 1978-04-20 Packing material consisting of a foil-like material with flow surfaces for "troughs" for mass and heat exchange Expired JPS5811558B2 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CH594977A CH618006A5 (en) 1977-05-12 1977-05-12

Publications (2)

Publication Number Publication Date
JPS5415554A JPS5415554A (en) 1979-02-05
JPS5811558B2 true JPS5811558B2 (en) 1983-03-03

Family

ID=4302002

Family Applications (1)

Application Number Title Priority Date Filing Date
JP53047167A Expired JPS5811558B2 (en) 1977-05-12 1978-04-20 Packing material consisting of a foil-like material with flow surfaces for "troughs" for mass and heat exchange

Country Status (14)

Country Link
US (1) US4186159A (en)
JP (1) JPS5811558B2 (en)
AU (1) AU518077B2 (en)
BR (1) BR7802956A (en)
CA (1) CA1093067A (en)
CH (1) CH618006A5 (en)
DE (2) DE2722556B2 (en)
ES (1) ES243474Y (en)
FR (1) FR2390201A1 (en)
GB (1) GB1604354A (en)
IT (1) IT1095802B (en)
MX (1) MX5488E (en)
NL (1) NL169784C (en)
SE (1) SE437475B (en)

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Also Published As

Publication number Publication date
AU518077B2 (en) 1981-09-10
GB1604354A (en) 1981-12-09
CH618006A5 (en) 1980-06-30
CA1093067A (en) 1981-01-06
ES243474U (en) 1980-01-16
IT1095802B (en) 1985-08-17
AU3597678A (en) 1979-11-15
SE7805339L (en) 1978-11-13
FR2390201B1 (en) 1980-02-08
DE2722556B2 (en) 1979-03-15
MX5488E (en) 1983-08-26
NL169784B (en) 1982-03-16
JPS5415554A (en) 1979-02-05
NL169784C (en) 1982-08-16
DE7804885U1 (en) 1978-11-02
NL7803456A (en) 1978-11-14
BR7802956A (en) 1978-12-26
IT7823043A0 (en) 1978-05-05
FR2390201A1 (en) 1978-12-08
ES243474Y (en) 1980-06-16
US4186159A (en) 1980-01-29
SE437475B (en) 1985-03-04
DE2722556A1 (en) 1978-11-16

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